WO2013015865A1 - Colonne à bulles en cercle roulant de type sels fondus, réacteurs l'utilisant et procédés associés - Google Patents

Colonne à bulles en cercle roulant de type sels fondus, réacteurs l'utilisant et procédés associés Download PDF

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Publication number
WO2013015865A1
WO2013015865A1 PCT/US2012/038251 US2012038251W WO2013015865A1 WO 2013015865 A1 WO2013015865 A1 WO 2013015865A1 US 2012038251 W US2012038251 W US 2012038251W WO 2013015865 A1 WO2013015865 A1 WO 2013015865A1
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WO
WIPO (PCT)
Prior art keywords
conduit
crucible
reactor
downtube
salt bath
Prior art date
Application number
PCT/US2012/038251
Other languages
English (en)
Inventor
Terry D. Turner
Bradley C. Benefiel
Dennis N. Bingham
Kerry M. Klingler
Bruce M. Wilding
Original Assignee
Battelle Energy Alliance, Llc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Battelle Energy Alliance, Llc filed Critical Battelle Energy Alliance, Llc
Priority to KR1020147004465A priority Critical patent/KR20140079760A/ko
Priority to EP12818387.8A priority patent/EP2734604A4/fr
Priority to AU2012287489A priority patent/AU2012287489A1/en
Priority to MX2014000586A priority patent/MX2014000586A/es
Priority to CN201280036148.XA priority patent/CN103842479B/zh
Priority to BR112014001149A priority patent/BR112014001149A2/pt
Priority to CA2841245A priority patent/CA2841245A1/fr
Priority to IN88DEN2014 priority patent/IN2014DN00088A/en
Publication of WO2013015865A1 publication Critical patent/WO2013015865A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/348—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents by direct contact with heat accumulating liquids, e.g. molten metals, molten salts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/005—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out at high temperatures in the presence of a molten material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2455—Stationary reactors without moving elements inside provoking a loop type movement of the reactants
    • B01J19/246—Stationary reactors without moving elements inside provoking a loop type movement of the reactants internally, i.e. the mixture circulating inside the vessel such that the upward stream is separated physically from the downward stream(s)
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J7/00—Apparatus for generating gases
    • B01J7/02—Apparatus for generating gases by wet methods
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00157—Controlling the temperature by means of a burner
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02—Apparatus characterised by their chemically-resistant properties
    • B01J2219/025—Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0277—Metal based
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0211—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step
    • C01B2203/0216—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step containing a non-catalytic steam reforming step

Definitions

  • the present invention relates generally to reactors and systems used in the production of gasses and, more particularly, components and methods used in reactors such as alkaline metal reactors.
  • Hydrocarbon based fuels including petroleum products, natural gas, etc.
  • Hydrocarbon based fuels have been, and remain, a major source of global energy production.
  • These research and development efforts have included the search for improved techniques, systems and methods for producing energy from existing, known energy sources. For example, efforts have been made regarding the ability to extract oil located in geophysical locations that are difficult to reach using conventional technology. Additionally, efforts have been made to make existing energy processes more efficient, more cost effective, and more environmentally friendly.
  • Embodiments of the present invention are related reactors used in the production of gasses as well as systems and processes in which the reactors may be used. Additionally, various embodiments of the present invention are related to components used in reactors.
  • a reactor is provided.
  • the reactor includes a furnace and a crucible positioned for heating by the furnace, the crucible defining an interior volume.
  • a downtube is disposed at least partially within the interior crucible, wherein the downtube includes a conduit having an inlet at a first end and an outlet at a second end.
  • the downtube further includes at least one opening formed in the conduit between the first end and the second end. The outlet and the at least one opening are configured to provide a recirculation path for any liquid material contained within the crucible.
  • the at least one opening may be tapered at one end thereof.
  • the at least one opening may include a plurality of openings within the conduit between the first and second ends.
  • the cross-sectional area of the downtube, as taken substantially perpendicular to a longitudinal axis, is approximately half of the cross-sectional area of the crucible, as taken substantially perpendicular to the axis.
  • a plurality of guide members may be coupled to the conduit to maintain the downtube in a desired position within the crucible.
  • a flow diversion structure may be associated with the conduit to direct any fluid flowing through the outlet in a desired direction or pattern.
  • an inlet is provided at the lower end of the crucible for the introduction of an oxidizing material.
  • a porous disc or screen may be positioned within the bottom of the crucible so that when the oxidizing material is introduced into the liquid contained within the crucible, a plurality of gas bubbles are formed within the liquid.
  • a gas processing system in accordance with another embodiment of the present invention, includes a supply of oxidizing material, a supply of hydrocarbon material and a reactor.
  • the reactor includes a furnace and a crucible positioned for heating by the furnace.
  • the crucible defines an interior volume and contains a catalyst material therein.
  • a downtube is disposed at least partially within the interior crucible along an axis.
  • the downtube includes a conduit having a first end, a second end and at least one opening between the first end and the second end.
  • the first end of the conduit is in fluid communication with the supply of hydrocarbon material and the second end provides an outlet into the interior volume of the crucible.
  • the outlet and the at least one opening define a recirculation path for the catalyst material within the crucible.
  • the supply of oxidizing material may be coupled with an inlet formed in a lower portion of the crucible.
  • a porous structure may be placed in the lower portion of the crucible such that the oxidizing material first passes through the porous structure and then into the catalyst material contained within the crucible as a plurality of gas bubbles.
  • the catalyst material of the system includes a salt such as, for example, sodium carbonate.
  • the supply of hydrocarbon material may include residual bitumen and the supply of oxidizing material may include water.
  • a downtube for use in the interior volume of a crucible of a reactor.
  • the downtube comprises a conduit having a first end and a second end.
  • a flow diversion structure is located adjacent the second end of the conduit and coupled to the conduit.
  • a plurality of guide members may be coupled with the conduit and extend radially outward from the conduit.
  • a splash guard may be coupled with the conduit and located between the at least one opening and the first end of the conduit.
  • the flow diverter may exhibit a substantially spherical geometry.
  • a method for controlling a reaction within a reactor.
  • the method comprises providing a salt bath within a crucible, introducing a hydrocarbon material into the salt bath through a conduit disposed at least partially within the crucible, introducing an oxidizing material into the salt bath at a bottom portion of the crucible, and providing a recirculation path through the conduit for the salt bath.
  • the method may include providing one or more openings in the conduit and flowing the salt bath through the opening and back through the conduit.
  • the oxidizing material may be introduced into the salt bath at a location near the bottom of the crucible as a plurality of bubbles, causing the salt bath to rise and flow into the opening in the conduit.
  • providing a salt bath may include providing sodium carbonate, while the oxidizing material may be provided as water and the hydrocarbon material may be provided as residual bitumen.
  • FIG. 1 is a schematic diagram showing a system including a reactor in accordance with an embodiment of the present invention
  • FIG. 2 is a perspective view of a reactor in accordance with an embodiment of the present invention.
  • FIG. 3 is a perspective view of the reactor shown in FIG. 1 showing a partial cross- section of one of the reactor's components;
  • FIG. 4 is a perspective view of a component that may be used in the reactor shown in FIGS. 2 and 3 in accordance with an embodiment of the present invention
  • FIG. 5 is a perspective view of a component that may be used in the reactor shown in
  • FIGS. 2 and 3 in accordance with an embodiment of the present invention
  • FIG. 6 is a schematic diagram showing the flow of materials within a reactor in accordance with an embodiment of the present invention.
  • FIG. 7 is a perspective view of reactor components according to an embodiment of the present invention
  • FIG. 8 is a perspective view of a reactor component according to an embodiment of the present invention.
  • FIG. 9 is a cross-sectional view of various reactor components in accordance with an embodiment of the present invention.
  • the present disclosure describes reactors and that may be used in extracting an energy source (e.g., hydrogen or other gases) from a given material.
  • an energy source e.g., hydrogen or other gases
  • Various components and methods associated with such reactors are also set forth herein.
  • One embodiment of the present invention described herein includes an alkaline metal reactor that processes materials in a manner referred to as alkaline metal reforming (AMR).
  • AMR alkaline metal reforming
  • various aspects of the described inventions may be applicable to a spectrum of energy conversion.
  • Feed materials generally include an oxidizing material and some form of hydrocarbon, though straight carbon is also useable.
  • the hydrocarbon material may include a residual bitumen material that is sometimes referred to as "resid.”
  • Resid material may also sometimes be referred to as vacuum residuum (VR).
  • Resid or VR materials are similar to road tar or asphalt and may produced during the vacuum distillation of crude oil. These materials are generally perceived has having a low economic value. Resid composition is largely carbon with a small percentage of hydrogen, even less sulfur and other trace elements as will be recognized by those of ordinary skill in the art.
  • used waste products and water may be fed into an alkali metal salt bath at high temperatures.
  • the resulting chemistry reaction will produce hydrogen, carbon monoxide, and carbon dioxide, along with a few other less significant gases.
  • a high temperature furnace may be used to heat a crucible containing the salt bath. Once the desired temperatures are reached, both the resid and water are introduced into the salt bath, which acts as a catalyst to produce the desired gas products.
  • the resulting gases can be separated and marketed as pure gases, i.e. hydrogen, carbon monoxide, and carbon dioxide. Alternately, the gases can be combined into a synthesis gas (syngas) used to produce fertilizers, chemicals, fuels, and other products.
  • synthesis gas syngas
  • the system 100 includes a source or supply of an oxidizing material 102.
  • the supply of oxidizing material 102 may include conditioned water that is maintained with a desired chemistry and at a desired temperature and pressure.
  • the system 100 additionally includes a source or supply of hydrocarbon material 104.
  • the supply of hydrocarbon material 104 may include resid material. In other embodiments, different oxidizing and hydrocarbon materials may be utilized.
  • the source of hydrocarbon material 104 may be maintained in specified conditions (e.g., temperature and pressure) in preparation for introduction into the reactor 106.
  • the reactor 106 may include a molten bath of salt or other material into which the oxidizing material and the hydrocarbon material will be introduced for reaction therewith.
  • the molten salt may include sodium carbonate
  • the hydrocarbon may be supplied as a resid material
  • the oxidizer may include water in steam form.
  • the chemical reaction that takes place within the reactor 106 produces gasses, liquids and solids.
  • using water and resid materials as reaction components to be introduced into a molten salt bath of sodium carbonate sodium hydroxide will be generated from the interaction of sodium carbonate and steam.
  • the sodium hydroxide, carbon, and water will then react to generate sodium carbonate and hydrogen.
  • the hydrogen, along with other reaction products, will leave the salt bath as a gas for further processing while the sodium carbonate will remain in the salt bath for subsequent reactions.
  • Various separation and treatment systems 108 may be used to separate and treat the products obtained from the reaction within the crucible 1 10 and to provide desired usable products such as, for example, hydrogen, methane, and other gasses. Water, salt and other products may also be separated out and recycled back to the reactor 106.
  • Various controls may be used in association with the system such as described, for example, in the previously incorporated U.S. Patent Application entitled SYSTEM AND PROCESS FOR THE
  • FIG. 2 shows a perspective view of the reactor 106 while FIG. 3 shows the same reactor 106 with one of the components depicted being "split" in cross- section to show additional details.
  • the reactor 106 includes a crucible 110 disposed within a furnace 1 12 that is mounted to a frame 114.
  • the furnace 112 may include a commercially available furnace such as, for example, a model XST-6-0-24-3C, three zone, hinged vertical tube furnace available from Carbolite, Inc., of Watertown, WI.
  • the furnace 1 12 may be configured to heat the crucible and its contents to a temperature of approximately 900°C to approximately 930°C or greater within a desired time period.
  • the furnace 112 may include multiple zones, shown as zones 116A-1 16C (FIG. 3) that are individually controllable to enable focused heating at specified locations along the length of the crucible 1 10. While three different zones 1 16A-116C are shown in FIG. 3, furnaces with more or fewer zones may be utilized.
  • a lifting mechanism 1 18 may be associated with the frame 114 to position and hold the crucible 110 at a desired elevation relative to the furnace 1 12.
  • the lifting mechanism 118 may also be configured to lift the crucible out of the furnace 112 when desired for cleaning, repair or replacement.
  • the crucible 1 10 may be formed as a substantially cylindrical member.
  • the crucible 110 may be formed from 304 stainless steel pipe having a cap 120 at one end and a flange 122 at the other end for connection with input and output systems.
  • the crucible 1 10 may be approximately 3 feet long and formed of 3 inch or 5 inch schedule 10 pipe.
  • An exhaust gas spool 124 is coupled with the upper flange 122 of the crucible 110.
  • the spool 124 may be configured with one or more gas outlets 126 to exhaust gasses produced by reactions taking place within the crucible 110.
  • the spool 124 may be configured to support internal components (e.g., a downtube structure) such as will be described in further detail below.
  • One or more inlets 130 may be associated with the spool for receiving process materials such as the hydrocarbon material (e.g., resid).
  • process materials such as the hydrocarbon material (e.g., resid).
  • the spool 124, the inlets 130 and outlets 126 may be covered with an insulating material or even wrapped with a heating element (e.g., tubing conveying a thermally conductive medium, electrical heat tape or other heating devices) to assist in maintaining any fluids flowing therethrough at a desired temperature.
  • a heating element e.g., tubing conveying a thermally conductive medium, electrical heat tape or other heating devices
  • Another inlet 132 may be located at the bottom of the crucible 1 10, such as in the end cap 120, to introduce other process materials (e.g., an oxidizing material such as water in steam form) into the crucible 110.
  • the piping and other components associated with the inlet 132 at the bottom of the crucible 110 may be insulated or heated to improve thermal performance of the system. Referring to FIG.
  • FIG. 4 shows a perspective view of a tube structure, referred to generally herein as a downtube 140.
  • the downtube 140 is used in introducing the resid material into the salt bath contained within the crucible 110. Additionally, as will be set forth below, the downtube 140 is configured to assist in controlling residence time of the process materials (e.g., water and resid) within the salt bath to provide enhanced reactions within the crucible 110 by providing a recirculation path within the crucible 110.
  • process materials e.g., water and resid
  • the downtube 140 includes a conduit 142 through which process materials are conveyed from the supply (e.g., the source of hydrocarbon material 104) into the crucible 110 and, thus, into the molten salt bath.
  • the conduit 142 may be a pipe or tube formed of a material that is able to withstand corrosive environments, high temperatures and high pressures.
  • the conduit 142, as well as other components of the downtube 140 may be formed of a stainless steel material.
  • a first end 144 of the downtube 140 may be structurally coupled with the spool 124 and placed in fluid connection with one or more inlets 130 of the spool 124.
  • a second end 146 of the downtube 140 may include a baffle or flow diverter 148 and a plurality of openings 150 formed near the flow diverter 148.
  • the openings may be sized, shaped and configured to provide free flow of the materials flowing through the downtube 140 into the crucible 110 while also minimizing the potential capture or trapping of any solids that may circulate through the downtube 140.
  • the flow diverter 148 may be formed as a substantially spherical member. However, the flow diverter 148 may be configured to exhibit other geometries including, for example, conical, convex or flat.
  • the flow diverter 148 is structured to divert the flow of process materials from their downward path through the conduit 142 and help disperse the process materials from the conduit 142 in a more radial direction near the bottom of the crucible 110.
  • the downtube 140 also includes a splash guard 152 coupled with the conduit 142.
  • the splash guard 152 is positioned on the conduit 142 based on an anticipated level of the various constituents within the crucible 110 during operation of the reactor 106 (e.g., the salt bath containing steam and resid components).
  • the splash guard 152 helps to prevent liquid from splashing from the salt bath onto upper surfaces of the crucible 110 which may be cooler than the salt bath.
  • the splashed liquid can solidify on the upper, interior surfaces of the crucible and, at a minimum, reduce the molten salt levels and possibly impeding or totally preventing gas flows.
  • One or more openings 154 may be formed within the splash guard 152 to enable gas to rise through the crucible 110 to the outlets 126 of the spool 124. Additionally, the splash guard 152 may be sized to provide a small space between itself and the crucible walls (e.g., forming an annulus) to also provide for passage of gasses.
  • weirs 156 may be formed in the conduit 142.
  • the weirs 156 may be located near the splash guard 152 and between the splash guard 152 and the second end 146 of the conduit 142.
  • the weirs 156 provide a recirculation path for the molten salt within the crucible.
  • the weirs 156 may include a lower section that is generally tapered.
  • the widening geometry of the weirs provides for an increased flow of recirculated molten salt into the conduit 142.
  • a plurality of fins or guide members 158 are coupled to the conduit 142 and extend radially outward therefrom.
  • the guide members 158 help to position the downtube 140 within the crucible 110 and keep it substantially centered along, or coaxial with, a longitudinal axis 160 of the crucible 110.
  • the guide members 158 may be positioned near the second end 146 of the conduit 142, such as adjacent the openings 150 and/or the flow diverter 148. However, the guide members 158 may be positioned at other longitudinal locations on the conduit 142.
  • Guide members 158 may be, for example, welded to the conduit 142, or otherwise attached using means and processes known to those of ordinary skill in the art which are able to withstand the temperatures, pressures and chemical conditions experienced within the crucible 1 10. As shown in FIG. 4, there may be three guide members 158 positioned at substantially equal angles about the conduit 142 (e.g., approximately 120° apart). However, other arrangements of guide members 158 may be used, including a different number, spacing or positioning of the guide members 158.
  • the cross-sectional area of the conduit 142 is approximately half that of the cross- section area of the crucible 110 when taken in the same direction.
  • the mass flow of the liquid flowing up the annulus defined between the conduit 142 and the inside surface of the crucible 1 10 may be approximately equal to the mass flow of liquid flowing down the conduit. It is noted that the apparent volume within the annulus will be larger because of the gas bubbles within the salt bath, the gas leaving the salt bath to exit the reactor 106 while the liquid is left to circulate back through the downtube 140.
  • ratios of the cross- sectional areas may be utilized depending, for example, on the types of materials, the mixture ratios of materials, and the viscosity of the materials within the crucible 110 as well as the desired recirculation rate through the conduit 142 of the downtube 140.
  • FIG. 5 another downtube 140' is shown in accordance with another embodiment of the present invention.
  • the downtube 140' is substantially similar to the downtube 140 shown in FIG. 4, having a conduit 142 with a first end 144, a second end 146, a splash guard 152 and weirs 154.
  • the flow diverter 148 is not in direct contact with the conduit 142. Rather, the flow diverter 148 is spaced from the second end 144 of the conduit 142 and the guide members 158 are coupled to both the conduit 142 and the flow diverter 148. Openings 150 are formed between the second end 146 of the conduit 142 and the flow diverter 148, defined in part by the guide members 158, as an outlet for material flowing through the conduit 142.
  • a reactant component e.g., resid
  • the conduit 142 of the downtube such as by injection under pressure as indicated by arrow 164.
  • the material may be introduced through the conduit 142 without pressure, such as by letting it drip.
  • the liquid level of the salt bath will be below the elevation of the weirs 156 as indicated by dashed lines in FIG. 6.
  • Another reactant component e.g., water
  • steam may be introduced through the inlet 132 at the bottom of the crucible 110 as indicated by arrow 166.
  • a porous disc 170 may be positioned inside the bottom of the crucible 110 above the inlet 132. Steam passing through the disc 170 will enter the salt bath within the crucible as a column of small bubbles 172.
  • the bubbles may be formed to exhibit approximately 1/16 inch diameters. The introduction of bubbles 172 into the salt bath causes the liquid level to rise.
  • the introduction of the gas bubbles 172 into the salt bath sets up a circulation of the salt bath that continually introduces the bath to new bubble sets.
  • the introduction of small bubbles 172 of steam (or other reaction component gasses) will increase the exposure or contact area of the oxidizing material with the liquid of the salt bath (including the resid or other reaction components) and will improve the efficiency of the chemical reactions (e.g., the conversion of sodium carbonate to sodium hydroxide).
  • the flow diverter 148 assists in dispersing materials flowing through the conduit 142 into the crucible in a more radial direction. Additionally, the flow diverter 148 also causes the steam or other reaction components flowing through the porous disc 170 to flow outward to mix with the other reaction components (e.g., the resid). Without the flow diverter 148, the reaction components introduced by the inlet 132 at the bottom of the crucible 110 would flow directly into the reaction components flowing out the bottom of the conduit 142 and the mixture of the components (and, thus, their reaction) would be less than desired. Additionally, without the flow diverter 148, gas bubbles could flow upward through the conduit 142 possibly hindering recirculation of the liquid through the conduit 142.
  • the rotating or recirculating action of the salt bath will cause a natural folding of the resid (or other reaction components) onto the catalyst materials, drawing it deeply into the molten bath.
  • the continued movement of the liquid will keep the sodium carbonate and hydroxide salts (produced by the chemical reactions) thoroughly mixed and will significantly reduce the opportunity for separation.
  • porous disc 170 is shown in accordance with one embodiment of the present invention.
  • the porous disc 170 may include, for example, a stainless steel mesh or other material configured to enable steam or other reaction components to flow therethrough and form a plurality of bubbles as described above.
  • the porous disc 170 may be exhibit a diameter of approximately 4 inches, a thickness of approximately 1/8 inch, and a pore size of approximately 0.5 micro inch.
  • the porous disc 170 may exhibit other configurations including different pore sizes.
  • the porous disc 170 may be formed as a substantially hollow body with an inlet 176 in communication with the interior of the hollow body. As shown in FIG. 9, the inlet 176 may extend through a bottom portion of the crucible 1 10 (e.g., the end cap 120), acting as the inlet 132 to the crucible 110 as discussed above with respect to FIG. 2. In another embodiment, the inlet 176 may be in communication with, and sealingly coupled with the inlet 132 of the crucible 110.
  • the porous disc 170 may be configured such that the upper wall 178 of the disc 170 is porous or allows fluid material to pass through.
  • other portions of the porous disc 170 such as the side wall 180, the bottom wall 182, or both, may be formed as porous structures in addition to, or in lieu of the top wall being 178 a porous structure.
  • the disc may be formed to substantially spread across the cross-sectional area of the crucible 110 as taken in a direction substantially perpendicular to the longitudinal axis 160 of the crucible 1 10.
  • the disc 170 may be formed to define an annulus or other space between the sidewall 180 and the wall of the crucible 1 10.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)

Abstract

Cette invention concerne des réacteurs pour la mise en œuvre d'une réaction chimique, ainsi que des composants, systèmes et procédés associés. Selon un mode de réalisation, le réacteur ci-décrit comprend un four et un creuset positionné de façon à être chauffé par le four. Le creuset peut contenir un bain de sels fondus. Un tube descendant se trouve au moins partiellement dans le creuset intérieur sur un de ses axes, ledit tube descendant comprenant un conduit ayant une première extrémité en communication avec une source de carbone et une sortie à sa seconde extrémité pour introduire le matériau carboné dans le creuset. Au moins une ouverture est formée dans le conduit entre la première et la seconde extrémité pour permettre la circulation par le conduit des composants de la réaction contenus dans le creuset. Un matériau oxydant destiné à réagir avec les autres matériaux peut être introduit par la partie de fond du creuset sous forme de bulles gazeuses.
PCT/US2012/038251 2011-07-21 2012-05-17 Colonne à bulles en cercle roulant de type sels fondus, réacteurs l'utilisant et procédés associés WO2013015865A1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
KR1020147004465A KR20140079760A (ko) 2011-07-21 2012-05-17 용용 염 롤링 버블 컬럼, 이를 사용한 반응기 및 관련 방법
EP12818387.8A EP2734604A4 (fr) 2011-07-21 2012-05-17 Colonne à bulles en cercle roulant de type sels fondus, réacteurs l'utilisant et procédés associés
AU2012287489A AU2012287489A1 (en) 2011-07-21 2012-05-17 Molten salt rolling bubble column, reactors utilizing same, and related methods
MX2014000586A MX2014000586A (es) 2011-07-21 2012-05-17 Columna de burbujas rodantes de sal fundida, reactores que utilizan la misma y metodos relacionados.
CN201280036148.XA CN103842479B (zh) 2011-07-21 2012-05-17 熔盐滚动鼓泡柱、用熔盐滚动鼓泡柱的反应器及相关方法
BR112014001149A BR112014001149A2 (pt) 2011-07-21 2012-05-17 coluna de bolhas rolantes de sal fundido, reatores que utilizam a mesma, e métodos relacionados
CA2841245A CA2841245A1 (fr) 2011-07-21 2012-05-17 Colonne a bulles en cercle roulant de type sels fondus, reacteurs l'utilisant et procedes associes
IN88DEN2014 IN2014DN00088A (fr) 2011-07-21 2012-05-17

Applications Claiming Priority (2)

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US13/188,202 US9187325B2 (en) 2011-07-21 2011-07-21 Molten salt rolling bubble column, reactors utilizing same and related methods
US13/188,202 2011-07-21

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WO2013015865A1 true WO2013015865A1 (fr) 2013-01-31

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EP (1) EP2734604A4 (fr)
JP (1) JP2014529351A (fr)
KR (1) KR20140079760A (fr)
CN (1) CN103842479B (fr)
AU (1) AU2012287489A1 (fr)
BR (1) BR112014001149A2 (fr)
CA (1) CA2841245A1 (fr)
IN (1) IN2014DN00088A (fr)
MX (1) MX2014000586A (fr)
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US9114984B2 (en) 2012-06-25 2015-08-25 Battelle Energy Alliance Llc System and process for upgrading hydrocarbons
US20150307792A1 (en) * 2014-04-29 2015-10-29 Dennis N. Bingham Method and apparatus for the production of fuel-gas, syngas and other constituent gas species
WO2018078062A1 (fr) * 2016-10-26 2018-05-03 Peter Ortmann Dispositif d'accumulation d'énergie et procédé d'accumulation d'énergie
CN113786797A (zh) * 2021-08-09 2021-12-14 中国原子能科学研究院 一种用于碱金属处理的反应装置及处理系统

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CN103842479B (zh) 2015-11-25
IN2014DN00088A (fr) 2015-05-15
KR20140079760A (ko) 2014-06-27
MX2014000586A (es) 2014-04-30
US9187325B2 (en) 2015-11-17
JP2014529351A (ja) 2014-11-06
CA2841245A1 (fr) 2013-01-31
EP2734604A1 (fr) 2014-05-28
CN103842479A (zh) 2014-06-04
EP2734604A4 (fr) 2015-04-22
US20130020232A1 (en) 2013-01-24
AU2012287489A1 (en) 2014-02-06
BR112014001149A2 (pt) 2017-02-21

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